EP2135937A1 - Système continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques - Google Patents

Système continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques Download PDF

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Publication number
EP2135937A1
EP2135937A1 EP08380179A EP08380179A EP2135937A1 EP 2135937 A1 EP2135937 A1 EP 2135937A1 EP 08380179 A EP08380179 A EP 08380179A EP 08380179 A EP08380179 A EP 08380179A EP 2135937 A1 EP2135937 A1 EP 2135937A1
Authority
EP
European Patent Office
Prior art keywords
production
culture
tube
phytoplankton
product
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP08380179A
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German (de)
English (en)
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EP2135937B1 (fr
Inventor
Bernard A. J. Stroïazzo-Mougin
Eduardo Rodriguez Verdu
Eloy Chapuli Fernandez
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Individual
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Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to DK08380179.5T priority Critical patent/DK2135937T3/en
Application filed by Individual filed Critical Individual
Priority to EP08380179.5A priority patent/EP2135937B1/fr
Priority to PT83801795T priority patent/PT2135937T/pt
Priority to HUE08380179A priority patent/HUE037653T2/hu
Priority to ES08380179.5T priority patent/ES2653848T3/es
Priority to AU2009259253A priority patent/AU2009259253A1/en
Priority to US12/999,890 priority patent/US20110195493A1/en
Priority to PCT/ES2009/070235 priority patent/WO2009153378A2/fr
Priority to CN200980132112.XA priority patent/CN102124093B/zh
Priority to BRPI0914146A priority patent/BRPI0914146A2/pt
Priority to ARP090102247A priority patent/AR072206A1/es
Publication of EP2135937A1 publication Critical patent/EP2135937A1/fr
Application granted granted Critical
Publication of EP2135937B1 publication Critical patent/EP2135937B1/fr
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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00—Bioreactors or fermenters specially adapted for specific uses
    • C12M21/02—Photobioreactors
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00—Constructional details, e.g. recesses, hinges
    • C12M23/02—Form or structure of the vessel
    • C12M23/06—Tubular
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00—Constructional details, e.g. recesses, hinges
    • C12M23/56—Floating elements
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M31/00—Means for providing, directing, scattering or concentrating light
    • C12M31/08—Means for providing, directing, scattering or concentrating light by conducting or reflecting elements located inside the reactor or in its structure
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M35/00—Means for application of stress for stimulating the growth of microorganisms or the generation of fermentation or metabolic products; Means for electroporation or cell fusion
    • C12M35/06—Magnetic means

Definitions

  • the object of the present invention is a continuous system for the generation of added value and energy resources.
  • An objective is to pass from this low energy density state to a high density state through a system for capturing sunlight and CO 2 to convert it into a continuous energy source using a magneto-hydro-photosynthetic catalyst, the latter being the actual system.
  • the amount of CO 2 emitted to the atmosphere is 10 kg. This is due to the fact that the CO 2 captured by the phytoplankton has generated in turn a power of 100 kW, therefore the balance of CO 2 emitted per kW produced is half.
  • the present invention describes a system in which not all the end product is intended for the production of fuels, but also for the production of a high nutritional value product.
  • the reactors that are currently used, either on an industrial or experimental scale, can be classified into two large groups:
  • the great drawback represented by this system is that, since it is completely open, the algae are susceptible of being contaminated by any organism that is introduced into the tank. Furthermore, the conditions of the system, such as temperature, evaporation of water from the culture medium, supply of CO 2 and luminosity are more difficult to control, the photochemical efficiency being low (high cell densities are not reached); therefore the depth of the tank is of a few millimeters, thus requiring large areas to reach high productions. The group of these factors makes this system not be the most suitable one for the mass cultivation of phytoplankton species.
  • the system described herein has the additional advantage that in the production step a magnetic field is applied which causes an acceleration of said step and, therefore, a substantial increase of the amount of obtained product.
  • the present invention relates to a novel system for obtaining energy resources by means of a system for capturing sunlight and CO 2 for the reconversion thereof into a continuous energy source using catalysts.
  • the system which will be described below, uses nutrients such as atmospheric CO 2 , carbon and nitrogen sources from different industrial sectors.
  • a total or partial recycling (depending on the application) of the CO 2 is achieved and therefore the net emission can be "zero", since the CO 2 generated can return to the system, thus nourishing the phytoplankton.
  • the water is reused after the separation step which will be described in more detail below.
  • the system has the advantage that the oxygen generated in one of its steps is reused as a raw material for a subsequent transformation of the obtained product.
  • Another advantage is that up until now there is no system in which a mass culture of photosynthetic strains is carried out as is done in the present invention.
  • Said system comprises at least:
  • the system also allows an amount of processing of the phytoplankton culture of up to 20000 liters/hour, preferably 5000 liters/hour.
  • the production modules for producing phytoplankton culture comprise a plurality of columns connected to one other, and wherein said columns in turn comprise:
  • the production modules for producing phytoplankton culture comprise four production columns for producing phytoplankton culture connected in parallel and/or in series.
  • the verticality of the production modules provides clear advantages compared to the traditional horizontal placement described in the state of the art, thus, for example, the capacity of discharging the oxygen which is generated in the culture is considerably improved.
  • Other inherent advantages are: a considerable improvement of the production, since the ratio of the volume per unit area increases; the necessary pumping requires a lower electric consumption, it being possible to stop the recirculation pump to prevent unnecessary energy consumptions during certain periods of the production step.
  • the modularity of the system is another considerable advantage, especially in actions of preventive maintenance and/or contamination of the phytoplankton culture, wherein only is necessary to treat the affected module and the rest of the system is not affected.
  • the pre-concentration means of the second separation means comprise at least one of the following systems or means:
  • the concentration means comprise at least one system selected from:
  • the drying means comprise, at least:
  • the continuous system for the generation of high nutritional value and energy resources in its preferred embodiment comprises at least:
  • the system also allows an amount of processing of the phytoplankton culture of up to 20000 liters/hour, preferably 5000 liters/hour.
  • the production modules (21) for producing phytoplankton culture (10) comprise a plurality of columns connected to one another, and wherein said columns in turn comprise:
  • the production modules (21) for producing phytoplankton culture (10) comprise four production columns (210) for producing phytoplankton culture connected in parallel and/or in series.
  • the system likewise comprises second separation means (50) connected to the outlet of the first production means (20), such that the water present in the latter is eliminated after an emptying step (30); and wherein said separation means comprise at least:
  • the system comprises third transformation means (60) for transforming the dry product obtained in the second means (50), such that an energy resource (70) and/or high nutritional value product (60) is obtained, wherein said third means comprise means selected from:
  • the pre-concentration means of the second separation means comprise at least one of the following systems or means:
  • the concentration means comprise at least one system selected from:
  • the drying means comprise, at least:
  • the CO 2 used for feeding the phytoplankton culture has its origin in a feedback from the transformation means.
  • the system in another practical embodiment incorporates wind generators, such that said wind generators generate the actual electricity for the use of the system, an excess energy accumulation being generated in the phytoplankton culture itself.
  • the system is installed in the sea, by means of floats and partially submerged.

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Molecular Biology (AREA)
  • Clinical Laboratory Science (AREA)
  • Cell Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Cultivation Of Seaweed (AREA)
EP08380179.5A 2008-06-20 2008-06-20 Procédé continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques Active EP2135937B1 (fr)

Priority Applications (11)

Application Number Priority Date Filing Date Title
EP08380179.5A EP2135937B1 (fr) 2008-06-20 2008-06-20 Procédé continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques
PT83801795T PT2135937T (pt) 2008-06-20 2008-06-20 Resumo
HUE08380179A HUE037653T2 (hu) 2008-06-20 2008-06-20 Folytonos üzemû eljárás magas tápértékû források és energiaforrások elõállítására
ES08380179.5T ES2653848T3 (es) 2008-06-20 2008-06-20 Procedimiento en continuo para la generación de un producto de valor nutricional elevado y de recursos energéticos
DK08380179.5T DK2135937T3 (en) 2008-06-20 2008-06-20 Continuous process for generating high nutritional value and energy resources
US12/999,890 US20110195493A1 (en) 2008-06-20 2009-06-18 Continuous system for converting co2 into high value-added and/or nutritional value products and energy resources
AU2009259253A AU2009259253A1 (en) 2008-06-20 2009-06-18 Continuous system for converting CO2 into products with high added and/or nutritional value and other energy resources
PCT/ES2009/070235 WO2009153378A2 (fr) 2008-06-20 2009-06-18 Système permettant la transformation continue de co2 en produits à haute valeur ajoutée et/ou nutritionnelle et en d'autres ressources énergétiques
CN200980132112.XA CN102124093B (zh) 2008-06-20 2009-06-18 用于将co2转化为高附加值和/或营养值产物及能源的连续系统
BRPI0914146A BRPI0914146A2 (pt) 2008-06-20 2009-06-18 sistema para tranformação de co2 em produtos de alto valor agregado e/ou nutricional e outros recursos de energia
ARP090102247A AR072206A1 (es) 2008-06-20 2009-06-19 Sistema en continuo de transformacion de co2 en productos de alto valor anadido y/o valor nutricional y otros recursos energeticos

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP08380179.5A EP2135937B1 (fr) 2008-06-20 2008-06-20 Procédé continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques

Publications (2)

Publication Number Publication Date
EP2135937A1 true EP2135937A1 (fr) 2009-12-23
EP2135937B1 EP2135937B1 (fr) 2017-09-27

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EP08380179.5A Active EP2135937B1 (fr) 2008-06-20 2008-06-20 Procédé continu pour la génération de valeur nutritionnelle élevée et de ressources énergétiques

Country Status (11)

Country Link
US (1) US20110195493A1 (fr)
EP (1) EP2135937B1 (fr)
CN (1) CN102124093B (fr)
AR (1) AR072206A1 (fr)
AU (1) AU2009259253A1 (fr)
BR (1) BRPI0914146A2 (fr)
DK (1) DK2135937T3 (fr)
ES (1) ES2653848T3 (fr)
HU (1) HUE037653T2 (fr)
PT (1) PT2135937T (fr)
WO (1) WO2009153378A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2915877B1 (fr) 2012-10-30 2016-09-28 Biosinkco2 Tech Lda. Procédé de production de biomasse et de produits dérivés de celle-ci par culture d'algues unicellulaires dans un milieu aqueux alimenté par un courant de co2, et installation conçue à cet effet

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US9556456B2 (en) * 2008-09-09 2017-01-31 Battelle Memorial Institute Production of bio-based materials using photobioreactors with binary cultures
US20120156669A1 (en) 2010-05-20 2012-06-21 Pond Biofuels Inc. Biomass Production
US8940520B2 (en) 2010-05-20 2015-01-27 Pond Biofuels Inc. Process for growing biomass by modulating inputs to reaction zone based on changes to exhaust supply
US8969067B2 (en) 2010-05-20 2015-03-03 Pond Biofuels Inc. Process for growing biomass by modulating supply of gas to reaction zone
US8889400B2 (en) 2010-05-20 2014-11-18 Pond Biofuels Inc. Diluting exhaust gas being supplied to bioreactor
US11512278B2 (en) 2010-05-20 2022-11-29 Pond Technologies Inc. Biomass production
US20120276633A1 (en) 2011-04-27 2012-11-01 Pond Biofuels Inc. Supplying treated exhaust gases for effecting growth of phototrophic biomass
US9534261B2 (en) 2012-10-24 2017-01-03 Pond Biofuels Inc. Recovering off-gas from photobioreactor
WO2014120087A1 (fr) * 2013-01-29 2014-08-07 Singapore Technologies Dynamics Pte Ltd Procédé pour la conception modulaire, la fabrication et l'assemblage de systèmes de biocolonne intégrés avec des sorties en aval multiples

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2915877B1 (fr) 2012-10-30 2016-09-28 Biosinkco2 Tech Lda. Procédé de production de biomasse et de produits dérivés de celle-ci par culture d'algues unicellulaires dans un milieu aqueux alimenté par un courant de co2, et installation conçue à cet effet

Also Published As

Publication number Publication date
CN102124093A (zh) 2011-07-13
AU2009259253A1 (en) 2009-12-23
US20110195493A1 (en) 2011-08-11
BRPI0914146A2 (pt) 2017-03-21
CN102124093B (zh) 2015-09-02
DK2135937T3 (en) 2018-01-08
ES2653848T3 (es) 2018-02-09
WO2009153378A3 (fr) 2010-10-21
EP2135937B1 (fr) 2017-09-27
WO2009153378A2 (fr) 2009-12-23
PT2135937T (pt) 2018-01-04
HUE037653T2 (hu) 2018-09-28
AR072206A1 (es) 2010-08-11

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